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Consider a following reaction carried out in a plug flow reactor. C₂H6 C₂H4 + H₂ C₂H6 + H₂ - 2 CH₂ C&H G The feed contains 85 mole% ethane and the balance inert. The fractional conversion of ethane is 0.5. A fluid medium comprising initially only ethane flows through the reactor with a mean axial velocity u = 2 m/s. Find differential equations for all components along the length of reactor.

Consider a following reaction carried out in a plug flow reactor. C₂H6 C₂H4 + H₂ C₂H6 + H₂ - 2 CH₂ C&H G The feed contains 85 mole% ethane and the balance inert. The fractional conversion of ethane is 0.5. A fluid medium comprising initially only ethane flows through the reactor with a mean axial velocity u = 2 m/s. Find differential equations for all components along the length of reactor.

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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Consider a following reaction carried out in a plug flow reactor. C₂H6C₂H4 + H₂ C₂H6 + H₂ 2 CH₂ cells The feed contains 85 mole% ethane and the balance inert. The fractional conversion of ethane is 0.5. A fluid medium comprising initially only ethane flows through the reactor with a mean axial velocity u = 2 m/s. Find differential equations for all components along the length of reactor. 1
Transcribed Image Text:Consider a following reaction carried out in a plug flow reactor. C₂H6C₂H4 + H₂ C₂H6 + H₂ 2 CH₂ cells The feed contains 85 mole% ethane and the balance inert. The fractional conversion of ethane is 0.5. A fluid medium comprising initially only ethane flows through the reactor with a mean axial velocity u = 2 m/s. Find differential equations for all components along the length of reactor. 1
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